首页> 外国专利> METHOD FOR SEPARATING PHENOL FROM STREAMS CONTAINING PHENOL THAT HAVE BEEN OBTAINED DURING THE PRODUCTION OF BISPHENOL A

METHOD FOR SEPARATING PHENOL FROM STREAMS CONTAINING PHENOL THAT HAVE BEEN OBTAINED DURING THE PRODUCTION OF BISPHENOL A

机译:从生产双酚A的过程中分离出含有苯酚的流中分离苯酚的方法

摘要

The invention relates to a method for the continuous separation of phenol from a sub-stream obtained during the production of bisphenol A, containing 40 to 90 wt. % phenol, 5 to 40 wt. % bisphenol A, in addition to 5 to 40 wt. % minor constituents, which occur during the conversion of phenol and acetone to bisphenol A. According to said method, a) the sub-stream is fed to a distillation column containing at least 5 theoretical separation stages, b) phenol is stripped via the head in the distillation column, c) a first part of the bottom product is evacuated from the process, and d) a second part of the bottom product is continuously transferred into a retention container, in which the minor constituents that are contained in the bottom product are at least partially isomerised at temperatures of 190 °C and a hydrodynamic residence time of at least 120 min, in the presence of an acidic catalyst and are then fed back to the distillation column. The mass flux of the part of the bottom product that is fed to the retention container amounts to more than 30 % of the mass flux of the sub-stream that is introduced into the column in step a).
机译:本发明涉及一种从生产双酚A的过程中得到的子流中连续分离苯酚的方法,该双流含有40至90wt。%的双酚A。 5至40重量%酚。除了5至40wt。%的双酚A外,还包括5wt。%的双酚A。在苯酚和丙酮转化为双酚A的过程中出现的少量次要成分。根据所述方法,a)将子流进料到包含至少5个理论分离阶段的蒸馏塔中,b)苯酚通过塔顶汽提在蒸馏塔中,c)将底部产物的第一部分从工艺中抽空,d)将底部产物的第二部分连续转移到保留容器中,其中底部产物中所含的次要成分在酸性催化剂的存在下,在> 190℃的温度和至少120分钟的流体力学停留时间下,将它们至少部分异构化,然后将其送回到蒸馏塔中。送入保留容器的部分底部产物的质量通量等于在步骤a)中引入塔中的子物流的质量通量的30%以上。

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